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Acid mine drainage neutralization in a pilot sequencing batch reactor using limestone from a paper and pulp industry

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dc.contributor.author Vadapalli, VRK
dc.contributor.author Zvimba, JN
dc.contributor.author Mathye, M
dc.contributor.author Fischer, H
dc.contributor.author Bologo, L
dc.date.accessioned 2016-02-23T09:33:52Z
dc.date.available 2016-02-23T09:33:52Z
dc.date.issued 2015-10
dc.identifier.citation Vadapalli, VRK, Zvimba, JN, Mathye, M, Fischer, H and Bologo, L. 2015. Acid mine drainage neutralization in a pilot sequencing batch reactor using limestone from a paper and pulp industry. Environmental Technology, Vol. 36(19), pp. 2515-2523 en_US
dc.identifier.issn 0959-3330
dc.identifier.uri http://www.tandfonline.com/doi/pdf/10.1080/09593330.2015.1036786
dc.identifier.uri http://hdl.handle.net/10204/8431
dc.description Copyright: 2015 Taylor & Francis. This is a post-print version. Due to copyright restrictions, the attached PDF file only contains the post-print version of the full text item. For access to the full text item, please consult the publisher's website. The definitive version of the work is published in Environmental Technology, Vol. 36(19), pp. 2515-2523 en_US
dc.description.abstract This study investigated the implications of using two grades of limestone from a paper and pulp industry for neutralization of acid mine drainage (AMD) in a pilot sequencing batch reactor (SBR). In this regard, two grades of calcium carbonate were used to neutralize AMD in a SBR with a hydraulic retention time (including settling) of 100 min and a sludge retention time of 360 min, by simultaneously monitoring the Fe(II) removal kinetics and overall assessment of the AMD after treatment. The Fe(II) kinetics removal and overall AMD treatment were observed to be highly dependent on the limestone grade used, with Fe(II) completely removed to levels lower than 50 mg/L in cycle 1 after 30 min using high quality or pure paper and pulp limestone. On the contrary, the other grade limestone, namely waste limestone, could only achieve a similar Fe(II) removal efficiency after four cycles. It was also noticed that suspended solids concentration plays a significant role in Fe(II) removal kinetics. In this regard, using pure limestone from the paper and pulp industry will have advantages compared with waste limestone for AMD neutralization. It has significant process impacts for the SBR configuration as it allows one cycle treatment resulting in a significant reduction of the feed stock, with subsequent generation of less sludge during AMD neutralization. However, the use of waste calcium carbonate from the paper and pulp industry as a feed stock during AMD neutralization can achieve significant cost savings as it is cheaper than the pure limestone and can achieve the same removal efficiency after four cycles. en_US
dc.language.iso en en_US
dc.publisher Taylor & Francis en_US
dc.relation.ispartofseries Workflow;15600
dc.subject Fe(II) en_US
dc.subject Acid mine drainage en_US
dc.subject Limestone en_US
dc.subject Sequencing batch reactor en_US
dc.subject Sludge en_US
dc.title Acid mine drainage neutralization in a pilot sequencing batch reactor using limestone from a paper and pulp industry en_US
dc.type Article en_US
dc.identifier.apacitation Vadapalli, V., Zvimba, J., Mathye, M., Fischer, H., & Bologo, L. (2015). Acid mine drainage neutralization in a pilot sequencing batch reactor using limestone from a paper and pulp industry. http://hdl.handle.net/10204/8431 en_ZA
dc.identifier.chicagocitation Vadapalli, VRK, JN Zvimba, M Mathye, H Fischer, and L Bologo "Acid mine drainage neutralization in a pilot sequencing batch reactor using limestone from a paper and pulp industry." (2015) http://hdl.handle.net/10204/8431 en_ZA
dc.identifier.vancouvercitation Vadapalli V, Zvimba J, Mathye M, Fischer H, Bologo L. Acid mine drainage neutralization in a pilot sequencing batch reactor using limestone from a paper and pulp industry. 2015; http://hdl.handle.net/10204/8431. en_ZA
dc.identifier.ris TY - Article AU - Vadapalli, VRK AU - Zvimba, JN AU - Mathye, M AU - Fischer, H AU - Bologo, L AB - This study investigated the implications of using two grades of limestone from a paper and pulp industry for neutralization of acid mine drainage (AMD) in a pilot sequencing batch reactor (SBR). In this regard, two grades of calcium carbonate were used to neutralize AMD in a SBR with a hydraulic retention time (including settling) of 100 min and a sludge retention time of 360 min, by simultaneously monitoring the Fe(II) removal kinetics and overall assessment of the AMD after treatment. The Fe(II) kinetics removal and overall AMD treatment were observed to be highly dependent on the limestone grade used, with Fe(II) completely removed to levels lower than 50 mg/L in cycle 1 after 30 min using high quality or pure paper and pulp limestone. On the contrary, the other grade limestone, namely waste limestone, could only achieve a similar Fe(II) removal efficiency after four cycles. It was also noticed that suspended solids concentration plays a significant role in Fe(II) removal kinetics. In this regard, using pure limestone from the paper and pulp industry will have advantages compared with waste limestone for AMD neutralization. It has significant process impacts for the SBR configuration as it allows one cycle treatment resulting in a significant reduction of the feed stock, with subsequent generation of less sludge during AMD neutralization. However, the use of waste calcium carbonate from the paper and pulp industry as a feed stock during AMD neutralization can achieve significant cost savings as it is cheaper than the pure limestone and can achieve the same removal efficiency after four cycles. DA - 2015-10 DB - ResearchSpace DP - CSIR KW - Fe(II) KW - Acid mine drainage KW - Limestone KW - Sequencing batch reactor KW - Sludge LK - https://researchspace.csir.co.za PY - 2015 SM - 0959-3330 T1 - Acid mine drainage neutralization in a pilot sequencing batch reactor using limestone from a paper and pulp industry TI - Acid mine drainage neutralization in a pilot sequencing batch reactor using limestone from a paper and pulp industry UR - http://hdl.handle.net/10204/8431 ER - en_ZA


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